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    • 4. 发明专利
    • SEWAGE TREATMENT BY OZONE INJECTION AND DEVICE THEREFOR
    • JPH09234478A
    • 1997-09-09
    • JP4445696
    • 1996-03-01
    • HITACHI LTD
    • YAHAGI TOSHIOWATANABE SHOJIBABA KENJIYODA MIKIOHARA NAOKIYAMAKOSHI NOBUYOSHI
    • B01D24/02C02F1/78
    • PROBLEM TO BE SOLVED: To efficiently execute the removal of waste gaseous ozone and to improve the water quality of treated water by transmitting the quality of a sewage and those of a treated water with a sand filter and a treated water with ozone to an arithmetic processor and controlling an ozone pouring quality so as to be appropriate to a present sewage quality with the arithmetic processor. SOLUTION: Each of water quality value signals 50, 51 and 52 of the sewage, the treated water with the sand filter and the treated water with the ozone measured respectively with water quality sensors 40, 41 and 42 is transmitted to a water quality measuring instrument 20, moreover, the water quality value is transmitted to the arithmetic processor 21 as a water quality judging signal 53. In the arithmetic processor 21, the ozone pouring quantity corresponding to an org. matter and the mixture of a soluble org. matter with a floating substance in the raw water (sewage) is calculated from the water quality value signal 50 of the sewage, and the ozone pouring quantity for the org. matter quantity which is the quantity by removing the mixture of the soluble org. matter with the floating substance using the sand filter is calculated from the water quality value signal 51 of treated water with the sand filter, and the differential value between both the pouring quantities is controlled as a suitable ozone pouring quantity. Accordingly, the quality of the treated water is improved.
    • 5. 发明专利
    • OPTIMUM OZONE INJECTION RATE CALCULATION APPARATUS AND OZONE INJECTION CONTROL APPARATUS
    • JPH08215690A
    • 1996-08-27
    • JP2495395
    • 1995-02-14
    • HITACHI LTD
    • YAMAKOSHI NOBUYOSHIYODA MIKIOHAGA TETSUROHARA NAOKI
    • C02F1/78
    • PURPOSE: To simply calculate an ozone amt. necessary for the reaction with an ozone consuming component in water to be treated with high accuracy by injecting ozone into water to be treated and comparison water prepared by removing an ozone consuming component from the water to be treated and measuring the difference between the concns. of dissolved ozone per a unit water amt. of both of them. CONSTITUTION: Water W to be treated is introduced into an ozone consuming component removing reaction tank 20 and ozone gas with predetermined concn. is injected into the reaction tank 20 from an ozonizer 2. The water to be treated and ozone are brought into contact with each other in the reaction tank 20 and treated water containing no ozone consuming component is introduced into a dissolved ozone removing reaction tank 25 and subsequently introduced into an ozone self-decomposing reaction tank 30. The amt. of waste ozone discharged to the open air from water is measured by a waste ozone concentration meter 32. The amt. of dissolved ozone contained in the water within the ozone self-decomposing reaction tank 30 is measured by a dissolved ozone concentration meter 35. Further, an ozone demand amt. is calculated on the basis of the difference between the amts. of dissolved ozone of both tanks 1, 30 in an ozone demand calculation part 40.
    • 7. 发明专利
    • OPERATION OF SAND FILTRATION TANK
    • JPH10192606A
    • 1998-07-28
    • JP359397
    • 1997-01-13
    • HITACHI LTD
    • YAHAGI TOSHIOWATANABE SHOJIYODA MIKIOHARA NAOKIYAMAKOSHI NOBUYOSHI
    • B01D24/02B01D24/46B01D24/48B01D29/60B01D29/62
    • PROBLEM TO BE SOLVED: To enable the performance of a sand filtration tank to be stabilized for a long time by setting the target value of the quantity of suspended substance to be captured at the time of a single filtering step and stopping a water circulation and switching the operation to a cleaning step when the calculated value of the quantity of the suspended substance captured in a sand layer reaches the set target value. SOLUTION: In a filtering step, the signal value 40 of untreated water quality and quantity and the signal value 41 of filtrate quality which are obtained by measurement with an influent quality sensor 20, a water quantity sensor 20' and a filtrate quality sensor 21, are sent to a calculation circuit 23 for calculating a suspended substance(SS) uptake quantity. In the calculation circuit 23, the SS uptake quantity to be obtained through a sand filtration tank 10 at the time of the filtering step is calculated. A calculated SS value 43 is entered to an interpretation circuit 24, and then is compared to the target value 47 of the SS uptake quantity (the SS quantity to be uptake is empirically calculated based on the quantity and quality of a filler and then the SS uptake quantity obtained through a single filtering step is previously entered). Further, when the deviation of the calculated SS value 43 from the target value 47 of the SS uptake quantity is below a specified value, the water supply to the filtering step is suspended and the operation is switched to a cleaning step.
    • 9. 发明专利
    • CONTROLLER FOR AMOUNT OF OZONE TO BE GENERATED FOR WATER TREATING FACILITY
    • JPH0873202A
    • 1996-03-19
    • JP21343094
    • 1994-09-07
    • HITACHI LTD
    • KAGEYAMA KOJIKOMATSU NAOTOHARA NAOKIYAMAKOSHI NOBUYOSHIWATANABE SHOJIBABA KENJIHAGA TETSURO
    • C02F1/78C01B13/10C01B13/11
    • PURPOSE: To adequately control the amt. of ozone to be generated with respect to a flow rate of inflow water by adding an arithmetic section for correcting the control target value on the flow rate of the inflow water to the fore stage of an existing control system for the ozone to be generated. CONSTITUTION: The raw water taken in from rivers, etc., is introduced to a flocculating and settling treatment 1, where a flocculating agent is injected into the raw water to remove sand and suspended materials. The raw water is automatically measured by a flow meter 3 and is introduced by a raw water pump 2 to an ozone contact basin 4. The gaseous raw material of an ozonizing gas is supplied by a blower 10 to an ozone generator 11 and the generated gaseous ozone is supplied as fine bubbles by a gas diffusion pipe 12 into the ozone contact basin 4, by which the dissolved org. materials in the water to be treated are oxidation decomposed. At this time, the ozone injection rate set by an ozone injection rate setter 6 is corrected by the measured value of the flowmeter 3 in the arithmetic section 7 for correcting the ozone injection rate and is transmitted to the arithmetic section 8 for the amt. of the ozone to be generated and the control section 9 for the amt. of the ozone to be generated. The effluent water from the ozone contact basin 4 enters a bioactive carbon treating device 5 where the dissolved org. materials are adsorbed away and the effluent water is subjected to the oxidation decomposition of microorganisms then to sterilization with chlorine. This water is distributed as city water.